EP0352048B1 - Process for synthesizing sucrose derivatives by regioselective reaction - Google Patents

Process for synthesizing sucrose derivatives by regioselective reaction Download PDF

Info

Publication number
EP0352048B1
EP0352048B1 EP89307228A EP89307228A EP0352048B1 EP 0352048 B1 EP0352048 B1 EP 0352048B1 EP 89307228 A EP89307228 A EP 89307228A EP 89307228 A EP89307228 A EP 89307228A EP 0352048 B1 EP0352048 B1 EP 0352048B1
Authority
EP
European Patent Office
Prior art keywords
sucrose
hydrocarbyl
reaction
distannoxane
benzoate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP89307228A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0352048A2 (en
EP0352048A3 (en
Inventor
Juan L. Navia
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Noramco LLC
Original Assignee
Noramco LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Noramco LLC filed Critical Noramco LLC
Publication of EP0352048A2 publication Critical patent/EP0352048A2/en
Publication of EP0352048A3 publication Critical patent/EP0352048A3/en
Application granted granted Critical
Publication of EP0352048B1 publication Critical patent/EP0352048B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H11/00—Compounds containing saccharide radicals esterified by inorganic acids; Metal salts thereof
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H13/00—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids
    • C07H13/02—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids by carboxylic acids
    • C07H13/04—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids by carboxylic acids having the esterifying carboxyl radicals attached to acyclic carbon atoms
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H13/00—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids
    • C07H13/02—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids by carboxylic acids
    • C07H13/04—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids by carboxylic acids having the esterifying carboxyl radicals attached to acyclic carbon atoms
    • C07H13/06—Fatty acids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H13/00—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids
    • C07H13/02—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids by carboxylic acids
    • C07H13/08—Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids by carboxylic acids having the esterifying carboxyl radicals directly attached to carbocyclic rings
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H23/00—Compounds containing boron, silicon, or a metal, e.g. chelates, vitamin B12

Definitions

  • the invention relates to a process for producing sucrose derivatives by a regioselective reaction, and can be used, for instance, to produce mono-substituted sucrose derivatives wherein the substituent is in the 6 position.
  • the invention also provides certain novel distannoxane compounds.
  • Sucrose is a disaccharide whose molecular structure is shown as Fig. 1. (In the figures showing the molecular structure of sucrose and derivatives thereof, the conformational formula is used. For convenience, the hydrogen atoms bonded to the carbon atoms in the two rings and the position numbers of the carbon atoms are shown only in Fig. 1.)
  • the sucrose molecule contains three primary hydroxyl groups and five secondary hydroxyl groups. Therefore, when it is desired to prepare derivatives of sucrose involving reaction of the hydroxyl groups, it can be a major synthesis problem to direct the reaction only to the desired hydroxyl groups.
  • the artificial sweetener 4,1′,6′-trichloro-4,1′,6′-trideoxy galacto sucrose is derived from sucrose by replacing the hydroxyls in the 4, 1′, and 6′ positions with chlorine.
  • the stereo configuration at the 4 position is reversed - hence the compound is a galacto sucrose.
  • the direction of the chlorine atoms to only the desired positions is a major synthesis problem, especially since the hydroxyls that are replaced are of differing reactivity (two are primary and one is secondary; the synthesis is further complicated by the fact that the primary hydroxyl in the 6 position is unsubstituted in the final product).
  • the preparation of this sweetener is only one illustration of the synthesis of sucrose derivatives wherein it is desired either to derivatize certain specific hydroxyl groups, and only such hydroxyl groups, or to derivatize only a specified number of the hydroxyls, perhaps in this latter case without particular regard to which particular hydroxyl(s) are derivatized.
  • the preparation of sucrose-based mono-ester surfactants is a commercial example of mono substitution on the sucrose molecule.
  • This invention provides a means for synthesizing sucrose compounds such as 6-substituted sucrose derivatives wherein the process of the invention is highly regioselective both with regard to directing the reaction strictly to the 6 position and to the preparation of mono-substituted derivatives only.
  • regioselective refers to a reaction that highly favors a single major product.
  • the process of the invention comprises reacting sucrose with a 1,3-di(hydrocarbyloxy)-1,1,3,3-tetra(hydrocarbyl)-distannoxane to produce a 1,3-di-(6-O-sucrose)-1,1,3,3-tetra(hydrocarbyl)distannoxane, a new class of compounds, which can then be reacted with an acylating agent to produce a sucrose-6-ester.
  • the 1,3-di(hydrocarbyloxy)-1,1,3,3-tetra(hydrocarbyl)distannoxane reactant is generated in situ , for example, by reacting a di(hydrocarbyl)tin oxide or equivalent reactant with an alcohol or phenol.
  • Figures 1-3 show structural formulas for sucrose, 1,3-di-(6-O-sucrose)-1,1,3,3-tetra(hydrocarbyl)distannoxane, and sucrose-6-esters, respectively.
  • the process of the invention comprises the reaction of a 1,3-di(hydrocarbyloxy)-1,1,3,3-tetra(hydrocarbyl)distannoxane [which will be referred to for brevity as a "di(hydrocarbyloxy)distannoxane”] with sucrose to form a 1,3-di-(6-O-sucrose)-1,1,3,3-tetra(hydrocarbyl)distannoxane [which will be referred to for brevity as a "di(hydrocarbyl)stannoxylsucrose”], which can then be reacted with an acylating agent to form a sucrose-6-ester.
  • a 1,3-di(hydrocarbyloxy)-1,1,3,3-tetra(hydrocarbyl)distannoxane which will be referred to for brevity as a "di(hydrocarbyl)stannoxylsu
  • the product of this reaction is 1,3-di-(6-O-sucrose)-1,1,3,3-tetrabutyldistannoxane (or dibutylstannoxylsucrose "DBSS”), a white solid.
  • the white solid is taken up in N,N-dimethylformamide (“DMF”), 100 ml, and 3.64 gm of benzoic anhydride (about 1 molar equivalent, based on sucrose), is added.
  • DMF N,N-dimethylformamide
  • benzoic anhydride about 1 molar equivalent, based on sucrose
  • sucrose-6-benzoate is insoluble in MeCl2, and it precipitates as a solid.
  • the solid contains about 3-6 wt% sucrose, with the balance being sucrose-6-benzoate.
  • the reaction is almost perfectly regioselective in that the yield of sucrose benzoate substituted in the 6 position is greater than 97 percent. (The percentage is that part of the total peak area from an HPLC elution profile that is attributed to sucrose-6-benzoate.
  • Other products are molecules that contain a UV chromophore that were not isolated or characterized.
  • dibutyltin oxide and sucrose were mixed and heated in refluxing methanol. It is believed that the methanol first reacts with the dibutyltin oxide to produce 1,3-dimethoxy-1,1,3,3-tetrabutyldistannoxane or "dimethoxydistannoxane").
  • the dimethoxydistannoxane is believed to be the species that reacts with the sucrose to form DBSS.
  • Analysis of DBSS is consistent with the conclusion that DBSS is a compound of the structure: Suc-O-Sn(Bu)2-O-Sn(Bu)2-O-Suc wherein Suc represents 6-O-sucrose (i.
  • Fig. 2 shows the molecular structure of the 1,3-di-(6-O-sucrose)-1,1,3,3-tetra(hydrocarbyl)distannoxanes that are produced by the process of the invention.
  • the " R " groups represent hydrocarbyl groups, which can be the same or different.
  • sucrose and di(hydrocarbyloxy)distannoxane reactants are used in proportions so as to produce the desired 1,3-di-(6-O-sucrose)-1,1,3,3-tetra(hydrocarbyl)distannoxane product.
  • the di(hydrocarbyloxy)distannoxane is generated in situ by the reaction of a di(hydrocarbyl)tin oxide with a lower alkanol such as methanol
  • the di(hydrocarbyl)tin oxide and sucrose are preferably used in the reaction in proportions such that there is at least one mol of di(hydrocarbyl)tin oxide per mol of sucrose.
  • dibutyltin oxide there can be used other di(hydrocarbyl)tin oxides in which the hydrocarbyl groups bonded to tin can be, individually, alkyl, cycloalkyl, aryl, or arylalkyl such as, for example, methyl, ethyl, propyl, butyl, octyl, benzyl, phenethyl, phenyl, naphthyl, cyclohexyl, and substituted phenyl.
  • the preferred hydrocarbyl groups are alkyl having up to eight carbon atoms.
  • a di(hydrocarbyl)tin dialkoxide, dihalide, diacylate, or other organic tin compound can be used as long as it generates the di(hydrocarbyloxy)distannoxane in situ .
  • the reaction is carried out in an organic liquid reaction medium that is a solvent for sucrose and the di(hydrocarbyloxy)distannoxane.
  • the reaction medium is preferably also a solvent for the compound(s) that are used to generate the di(hydrocarbyloxy)distannoxane. More preferably, the reaction medium is also one of the reactants that are used to generate the di(hydrocarbyloxy)distannoxane in situ .
  • a wide variety of aliphatic and cycloaliphatic alcohols or phenols can be used as the reaction medium.
  • the reaction between the di(hydrocarbyl)tin oxide (or equivalant reactant) and the alcohol or phenol under atmospheric reflux conditions it is often most economical to carry out the reaction between the di(hydrocarbyl)tin oxide (or equivalant reactant) and the alcohol or phenol under atmospheric reflux conditions.
  • lower alkyl primary alcohols are generally preferred.
  • the preferred reaction mediums are primary lower alkanols such as methanol, ethanol, n-propanol, n-butanol, n-pentanol, and n-hexanol.
  • Additional alcohols and phenols that may be used as the reactant/reaction medium include secondary alcohols such as isopropyl alcohol and other secondary alkanols, phenol, substituted phenols such as lower alkyl-substituted phenols, cyclohexanol and substituted cyclohexanols such as lower alkyl-substituted cyclohexanol.
  • secondary alcohols such as isopropyl alcohol and other secondary alkanols
  • phenol substituted phenols such as lower alkyl-substituted phenols
  • cyclohexanol and substituted cyclohexanols such as lower alkyl-substituted cyclohexanol.
  • Inert organic liquids such as toluene, xylene, and other hydrocarbons may also be used in the reaction, if desired.
  • the di(hydrocarbyloxy)distannoxane can be represented by the formula: R′-O-Sn(R)2-O-Sn(R)2-O-R′ wherein each R ′ individually represents alkyl, cycloalkyl, aryl, or aralkyl, and wherein each R individually represents a hydrocarbyl group, e. g., alkyl, cycloalkyl, aryl, or aralkyl.
  • the reaction between sucrose and the di(hydrocarbyloxy)distannoxane is carried out at a temperature and for a period of time sufficient to form the di(hydrocarbyl)stannoxylsucrose.
  • Illustrative reaction temperatures are within the range of from about 50° to about 150°C. It is most convenient to carry out the reaction at the normal (i. e., at atmospheric pressure) refluxing temperature of the reaction medium.
  • Illustrative reaction times are from about 1 to about 24 hours.
  • the di(hydrocarbyl)stannoxylsucrose is recovered by procedures that are analogous to those that are known in the art.
  • the reaction medium is removed, as by stripping off, which may be performed under reduced pressure if desired.
  • the product is a solid, which may be purified by recrystallization, if desired.
  • the di(hydrocarbyl)stannoxylsucrose product of the stripping procedure may be used directly without further purification in an acylation reaction. It is preferred to employ one molar equivalent of acylating agent in the reaction (the equivalence is based upon the molar equivalents of sucrose). In this context, one mol of benzoic anhydride would constitute one molar equivalent. A slight excess, e. g., from 1 to 5 mol% excess, of acylating agent may be used, if desired.
  • acylating agent to be used in the acylation reaction is dictated in part by the use to which the acylated product is to be put. For example, if the acyl group is being employed as a blocking group, as it would be in the preparation of the artificial sweetener as discussed above in the Background of the Invention section of this application, an acylating agent such as benzoic or acetic anhydride would be employed because it is inexpensive, the acyl group is readily removed at an appropriate stage of the synthesis, and it is stable to reactions that the acylated compound must undergo prior to removal of the acyl group.
  • the acylating agent used is the one that will generate the desired acyl group for the ester product.
  • the acylating agents that can be used are the various anhydrides and acid halides of benzoic and substituted benzoic acid (e.
  • alkanoic acids such as acetic acid, propionic acid, butyric acid, cyclohexanecarboxylic acid, long chain fatty acids, both saturated and unsaturated, such as stearic acid, oleic acid, linoleic acid, and the like, having up to, for example, 28 carbon atoms, unsaturated acids such as acrylic acid and methacrylic acid, substituted acids such chloroacetic acid, cyanoacetic acid, phenoxyacetic acid, and the like, and saturated and unsaturated dicarboxylic acids such as phthalic acid, maleic acid, glutaric acid, and the like.
  • alkanoic acids such as acetic acid, propionic acid, butyric acid, cyclohexanecarboxylic acid, long chain fatty acids, both saturated and unsaturated, such as stearic acid, oleic acid, linoleic acid, and the like, having up to, for example, 28 carbon atoms, unsaturated
  • the acylation reaction is carried out in an inert organic reaction vehicle such as DMF or other polar, aprotic compounds such as N-methylpyrrolidinone, dimethyl sulfoxide, and the like, that is a solvent for both reactants and reaction product.
  • the acylation reaction is carried out at a temperature and for a period of time sufficient to prepare the sucrose-6-ester product. Typical reaction temperatures are found within the range of from about 0°C to about 80°C. In the specific reaction discussed above, the reaction was carried out at room temperature (about 18-25°C). Typical reaction times are usually found within the range of from about 0.5 hour to about 48 hours.
  • the sucrose-6-ester product of the above reaction can be recovered by procedures that are analogous to recovery procedures that are known in the art. For instance, the reaction medium may be removed (as by stripping), and the reaction products may then be taken up in a liquid material that dissolves either the sucrose-6-ester or the by-product tin compound(s), but not both.
  • methylene chloride was used because it completely dissolves the tin compound(s) but not the sucrose-6-ester. After adding the methylene chloride, the sucrose-6-ester is recovered by filtration.
  • the sucrose-6-ester may be washed with moderately polar aprotic solvents such as acetonitrile or acetone to ensure essentially complete removal of the tin compound(s). Such solvents dissolve the tin compound(s), but little or no sucrose-6-ester.
  • moderately polar aprotic solvents such as acetonitrile or acetone to ensure essentially complete removal of the tin compound(s).
  • solvents dissolve the tin compound(s), but little or no sucrose-6-ester.
  • the molecular structure of the sucrose-6-ester product of the invention is represented by the formula shown in Fig. 3, wherein " Ac " represents an acyl group.
  • the tin compound(s) may be recovered from methylene chloride solution and recycled. This adds to the economies of the process of the invention.
  • DBSS 1,3-Di-(6-O-sucrose)-1,1,3,3-tetrabutyldistannoxane
  • Sucrose benzoate samples were analyzed by high performance liquid chromatography (HPLC). Sample components were separated on a reversed-phase, octadecylsilane HPLC column, with gradient elution from 10% methanol/90% 0.01M K2HPO4, pH 7.5 buffer to 69.5% methanol/30.5% buffer. Detection was by ultraviolet absorption at 254 nm. Samples were analyzed against a sucrose-6-benzoate standard of known composition and purity to determine percentage by weight.
  • sucrose-6-benzoate standard was prepared as described herein, recrystallized from acetonitrile to obtain a sample of high purity, and its structure was established by NMR analysis, which is given below.
  • Chromatographic purity was also calculated from the total chromatographic peak profile.
  • Sucrose laurates esters were analyzed on a reversed phase column using an isocratic mobile phase of 60% methanol/40% water. Refractive index detection was employed.
  • sucrose content of sucrose benzoate samples was determined by HPLC analysis. Sucrose was separated from the other sample components with an amine-bonded HPLC column, using an isocratic mobile phase of 85% acetonitrile/15% water. Refractive index detection was employed, and the sucrose peak in the sample was compared with that from a sucrose standard solution to allow quantitation of the sucrose content of the sample.
  • DBSS (57.3 g) and benzoic anhydride (24.9 g) were stirred together in dimethylformamide (580 ml) at 18-22°C for 23 hours.
  • the mixture was evaporated to a syrup.
  • a gummy mass was precipitated from the syrup by trituration with MeCl2:hexane (2:1, 300 ml); the supernatant was decanted away and the gummy residue was triturated in MeCl2 (160 ml), the solid was recovered by filtration, washed first with MeCl2 and then hexane, and then air dried to give 36.2 g of product of which 71 wt % was sucrose-6-benzoate.
  • sucrose-6-benzoate (11.2 wt-% sucrose; sucrose-6-benzoate is 90% of all UV absorbing material).
  • DBSS (5 g) in DMF (50 ml) was treated with acetic anhydride (1.02 g) at room temperature for 3 hrs, then the mixture was evaporated and the syrup was triturated with 50 ml of MeCl2. After 20 min the resulting solid was recovered by filtration, washed with MeCl2 and hexane, and air-dried to give 3.1 g of product containing 63.4 wt % sucrose-6-acetate and 3.8 wt % sucrose.
  • DBSS (5.73 g) in DMF (55 ml) was treated with glutaric anhydride (1.2 g) at room temperature for 3 hrs then at 40°C (oil bath) overnight. Additional glutaric anhydride (1 g) was added, and after 4 hrs at 40°C, methanol (10-15 ml) was added to destroy unreacted anhydride. The mixture was allowed to remain at room temperature overnight, and was then evaporated. The resulting syrup was triturated with MeCl2 (100 ml). The supernatant was decanted away, the process was repeated with two 80 ml portions of MeCl2, and the hygroscopic solid was recovered by filtration and then vacuum drying to give 4.3 g of crude product.
  • DBSS (5.73 g) was treated with lauric anhydride (3.9 g) in DMF (55 ml) at room temperature for 2 hrs and then at 40°C (oil bath) for 5 hrs.
  • the mixture was treated with additional lauric anhydride (1.1 g), and the reaction was continued for 2 hours and then quenched with methanol (10-15 ml) to destroy unreacted anhydride.
  • the mixture was evaporated, and the residue was treated with a mixture containing 70 ml of diethyl ether and 100 ml hexane.
  • the DBSS was dissolved in DMF (150 ml) with warming to about 40°C, and the solution was cooled to ambient temperature.
  • Benzoic anhydride (38.0 g, 1.15 mol equiv) was added and the resultant solution was stirred at room temperature for 3 hours at which time tlc (silica gel, eluant 15:10:2 chloroform:methanol:water) indicated the absence of benzoic anhydride and the presence of only a small amount of sucrose relative to sucrose monobenzoate.
  • the DMF was evaporated at high vacuum to afford a pale greenish-yellow oil (approximately 160 g), which was dissolved in acetone (500 ml) at 40°C and slowly cooled to room temperature.
  • the DBSS described above was dissolved in 400 ml of DMF and transferred to a 1000-ml, one-neck, round-bottom flask equipped with magnetic stir bar and argon inlet. The mixture was cooled in an ice bath, treated with 19.7 g (87.2 mmol) of benzoic anhydride, and allowed to warm and stir at room temperature for 12 hours under argon. Evaporation of the DMF (rotary evaporator, mechanical pump, 40°C bath temperature) provided a viscous oil which was treated with 250 ml of acetone and heated to about 50°C to produce a clear solution from which sucrose-6-benzoate readily crystallized on cooling to room temperature.
  • DMF rotary evaporator, mechanical pump, 40°C bath temperature
  • the product was filtered on a coarse-frit, sintered-glass filter, washed with acetone (2 x 100 ml), and vacuum dried (50°C, 0.5 mm, 16 hours) to produce 13.8 g of white solid shown by HPLC analysis to consists of 97.4% sucrose-6-benzoate.
  • the slurry was heated to 125°C with stirring over 0.5 hour, and the clear solution produced held at this temperature with stirring under argon for 2.5 hours.
  • the reaction mixture was then allowed to cool to 90°C, and 34.2 g (100 mmol) of sucrose was added.
  • the DMF solution (50.0 mmol DBSS in theory) was transferred to a 1000-ml, one-neck, round-bottom flask equipped with magnetic stir bar and argon inlet. The solution was cooled in an ice bath, treated with 24.9 g (110 mmol) of benzoic anhydride, and stirred for 8 hours at 0°C and then 12 hours at room temperature. The reaction was further processed as described in Example 8/Method A to provide 32.2 g of white solid shown by HPLC analysis to consist of 98.1% sucrose-6-benzoate.
  • the slurry was heated to 150°C (bath) over 0.5 hour, and the clear solution thus obtained held at this temperature for an additional 1.5 hours.
  • the heating bath was allowed to cool to 120°C, and the solution was treated with 3.42 g (10.0 mmol) of sucrose.
  • Diphenoxydistannoxane was prepared according to the method of W. J. Considine, et al., Can. J. Chem. , 41 , 1239 (1963).
  • the crude diphenoxydistannoxane (25.0 mmol in theory) was treated with 250 ml of DMF and 17.1 g (50.0 mmol) of sucrose and stirred at room temperature under argon.
  • the sucrose was observed to rapidly dissolve, while the crude diphenoxydistannoxane was seen to require several hours to enter solution.
  • the essentially clear solution was treated with 11.3 g (50.0 mmol) of benzoic anhydride with continued stirring at room temperature under argon, and the progress of the benzoylation monitored by silica gel tlc (15:10:2, chloroform-methanol-water).
  • reaction mixture was quenched with CH3OH (15 ml), and evaporated (rotary evaporator, vacuum pump, 55°C) to a gummy solid shown by HPLC to contain 1.51 g of sucrose-6-benzoate.
  • the acylation reaction using an acid chloride works best using a hindered tertiary amine present in the reaction mixture as an acid acceptor. However, the reaction will proceed with no amine present or with a non-hindered tertiary amine (such as triethylamine) present.
  • This Example illustrates an alternative way to generate the dimethoxy distannoxane reactant in situ .
  • the DBSS thus produced was treated at room temperature for 18 hours with 7.27 g (32.2 mmol) of benzoic anhydride in 20 ml of DMF. The solvent was then evaporated and the product worked up in the usual fashion with 100 ml of acetone to give 9.58 g of solid shown by HPLC analysis to contain 83.4% sucrose-6-benzoate.
  • This Example illustrates the use of a substituted alcohol to prepare the 1,3-di(hydrocarbyloxy)distannoxane reactant.
EP89307228A 1988-07-18 1989-07-17 Process for synthesizing sucrose derivatives by regioselective reaction Expired - Lifetime EP0352048B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US220641 1980-12-29
US07/220,641 US4950746A (en) 1988-07-18 1988-07-18 Process for synthesizing sucrose derivatives by regioselective reaction

Publications (3)

Publication Number Publication Date
EP0352048A2 EP0352048A2 (en) 1990-01-24
EP0352048A3 EP0352048A3 (en) 1991-09-04
EP0352048B1 true EP0352048B1 (en) 1994-11-30

Family

ID=22824357

Family Applications (1)

Application Number Title Priority Date Filing Date
EP89307228A Expired - Lifetime EP0352048B1 (en) 1988-07-18 1989-07-17 Process for synthesizing sucrose derivatives by regioselective reaction

Country Status (24)

Country Link
US (1) US4950746A (tr)
EP (1) EP0352048B1 (tr)
JP (1) JP2725710B2 (tr)
KR (1) KR0143234B1 (tr)
AR (1) AR245136A1 (tr)
AT (1) ATE114664T1 (tr)
AU (1) AU618107B2 (tr)
CA (1) CA1323625C (tr)
DE (1) DE68919566T2 (tr)
DK (1) DK170027B1 (tr)
ES (1) ES2065386T3 (tr)
FI (1) FI91874C (tr)
GR (1) GR1002250B (tr)
IE (1) IE65990B1 (tr)
IL (1) IL91004A (tr)
MX (1) MX172793B (tr)
NO (1) NO171855C (tr)
NZ (1) NZ229823A (tr)
PH (1) PH26098A (tr)
PT (1) PT91186B (tr)
RU (1) RU2041233C1 (tr)
TR (1) TR27628A (tr)
YU (1) YU47159B (tr)
ZA (1) ZA895427B (tr)

Families Citing this family (51)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5089608A (en) * 1990-03-23 1992-02-18 Mcneil-Ppc, Inc. Selective 6-acylation of sucrose mediated by cyclic adducts of dialkyltin oxides and diols
US5023329A (en) * 1990-04-23 1991-06-11 Noramco, Inc. Sucrose-6-ester production process
US5034551A (en) * 1990-04-23 1991-07-23 Noramco, Inc. Process for recovery of organotin esters from reaction mixtures containing the same and re-use of the recovered organotin compounds
GR910100356A (el) * 1990-08-27 1992-08-31 Mcneil Ppc Inc Καταλυόμενη μέ?οδος εστέρος-6-σακχαρόζης.
US5470969A (en) * 1990-08-27 1995-11-28 Mcneil-Ppc, Inc. Catalyzed sucrose-6-ester process
FR2670493A1 (fr) * 1990-12-13 1992-06-19 Isochem Sa Nouveaux composes monoesters du saccharose tels que les 2-0-acylsaccharoses et les 6-0-acylsaccharoses, ainsi que leurs procedes de synthese.
US5298611A (en) * 1993-03-12 1994-03-29 Mcneil-Ppc, Inc. Sucralose pentaester production
WO1996001832A1 (en) 1994-07-11 1996-01-25 The United States Of America, Represented By The Secretary Of The Department Of Agriculture Chemically synthesized sugar esters for the control of soft-bodied arthropods
US6608039B1 (en) 1994-07-11 2003-08-19 The United States Of America As Represented By The Secretary Of Agriculture Chemically synthesized sugar esters for the control of soft-bodied arthropods
US5498709A (en) 1994-10-17 1996-03-12 Mcneil-Ppc, Inc. Production of sucralose without intermediate isolation of crystalline sucralose-6-ester
ES2191745T3 (es) 1995-11-28 2003-09-16 Mcneil Ppc Inc Procedimiento de preparacion de 6-ester de sacarosa.
US6121430A (en) * 1998-12-28 2000-09-19 University Of Iowa Research Foundation Regiospecific synthesis of glucose-based surfactants
CN1245895C (zh) 2000-11-17 2006-03-22 塔特和莱利有限公司 含三氯蔗糖和丁磺氨钾的可熔混合物的甜味剂、含有它的食品以及它们的制备方法
EP1339728B1 (en) 2000-11-17 2013-02-27 Tate & Lyle Technology Limited Improved sucralose composition and process for the crystallization thereof
US6890581B2 (en) * 2002-04-05 2005-05-10 Tate & Lyle Public Limited Company Methods for buffer stabilized aqueous deacylation
US6943248B2 (en) 2003-04-30 2005-09-13 Tate & Lyle Public Limited Company Crystalline form of sucralose, and method for producing it
CN1176094C (zh) * 2003-05-23 2004-11-17 广东省食品工业研究所 一种三氯蔗糖的合成方法
US20050214425A1 (en) * 2004-03-23 2005-09-29 Roma Vazirani Sugar substitute prepared with nutritive and high-intensity sweeteners
US20090105470A1 (en) * 2005-02-22 2009-04-23 Pharmed Medicare Private Limited , A Corporation Tin Mediated Regioselective Synthesis of Sucrose-6-Esters
US7750146B2 (en) 2005-03-18 2010-07-06 Tate & Lyle Plc Granular sucralose
US20060247180A1 (en) * 2005-04-29 2006-11-02 Bergey James L Purgative composition and uses thereof
US20060276639A1 (en) * 2005-06-01 2006-12-07 Healthy Brands, Llc Conversion of sucralose-6-ester to sucralose
CN100418976C (zh) * 2006-04-03 2008-09-17 广州科宏食品添加物有限公司 一种三氯蔗糖的制备方法
CN101092438A (zh) * 2006-06-22 2007-12-26 南京莱因医药科技有限公司 6－o－苯甲酰三氯半乳型蔗糖四乙酯的制备方法
GB0702854D0 (en) * 2007-01-09 2007-03-28 Tate & Lyle Plc Method for the synthesis of sucrose-6-esters
US20080227971A1 (en) * 2007-01-19 2008-09-18 Leinhos Duane A Deacylation of sucralose-6-acylates
GB0702857D0 (en) * 2007-01-19 2007-03-28 Tate & Lyle Plc Improved sucralose production method
US20090076261A1 (en) * 2007-09-13 2009-03-19 Polymed Therapeutics, Inc. Novel process for preparing sucrose-6-esters
CN101245085B (zh) * 2007-12-19 2012-02-01 上海同辰生物科技有限公司 一种三氯蔗糖的合成及纯化工艺
US8436156B2 (en) * 2008-01-04 2013-05-07 Tate & Lyle Technology Limited Method for the production of sucralose
US7932380B2 (en) 2008-03-06 2011-04-26 Wanhe International (Group) Co. Ltd. Process for the preparation of sucralose
US8557976B2 (en) * 2008-03-13 2013-10-15 Tate & Lyle Technology Limited Microbial consortia and methods for their use
WO2009117317A1 (en) * 2008-03-20 2009-09-24 Tate & Lyle Technology Ltd Removal of acids from tertiary amide solvents
US8436157B2 (en) * 2008-03-26 2013-05-07 Tate & Lyle Technology Limited Method for the production of sucralose
US8497367B2 (en) * 2008-04-03 2013-07-30 Tate & Lyle Technology Limited Sucralose purification process
WO2009124113A1 (en) * 2008-04-03 2009-10-08 Tate & Lyle Technology Ltd. Extraction of less polar impurities from sucralose containing aqueous feed streams
US20090299055A1 (en) * 2008-04-03 2009-12-03 Tate & Lyle Technology Limited Purification of Sucralose Containing Feed Streams for Sucralose Crystallization
AR071134A1 (es) * 2008-04-03 2010-05-26 Tate & Lyle Technology Ltd Cristalizacion de sucralosa a partir de chorros que contienen sucralosa
CN101981044B (zh) * 2008-04-03 2014-08-06 塔特和莱利技术有限公司 碳水化合物浓度对三氯半乳蔗糖萃取效率的影响
GB2469157B (en) 2009-03-30 2011-07-06 John Kerr Process for removing dimethylamine during sucralose production
GB2469158B (en) * 2009-03-31 2011-09-28 Peter J Seaberg Base-assisted formation of tin-sucrose adducts
GB2471348B (en) 2009-06-22 2011-12-14 Tate & Lyle Technology Ltd A method for producing sucralose-6-acylate
GB2474311B (en) * 2009-10-12 2012-10-17 Tate & Lyle Technology Ltd Low temperature, single solvent process for the production of sucrose-6-ester
GB2474310B (en) * 2009-10-12 2012-02-29 Tate & Lyle Technology Ltd Process for the production of sucrose-6-ester
CN101759728B (zh) * 2010-01-08 2012-01-11 江苏巨邦制药有限公司 三氯蔗糖的生产及精制方法
GB201110520D0 (en) 2011-05-10 2011-08-03 Tate & Lyle Technology Ltd Extraction of carboxylic acids with tin compounds
CN105829332B (zh) 2013-12-16 2018-10-02 塔特和莱利技术有限公司 蔗糖-6-酯的氯化
GB2544217B (en) 2014-08-08 2020-03-25 Tate & Lyle Tech Ltd Chlorination of sucrose-6-esters
GB2536480B (en) 2015-03-17 2019-09-04 Tate & Lyle Tech Ltd DMF Distillation
WO2017091437A1 (en) 2015-11-24 2017-06-01 Archer Daniels Midland Company Organotin catalysts in esterification processes of furan-2,5-dicarboxylic acid (fdca)
GB2551591B (en) 2016-06-23 2019-08-07 Tate & Lyle Tech Ltd Liquid-liquid extraction of DMF

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4435440A (en) * 1976-01-08 1984-03-06 Tate & Lyle Limited Sweeteners
DE3065399D1 (en) * 1979-12-18 1983-11-24 Tate & Lyle Plc Crystalline 4,1',6'-trichloro-4,1',6'-trideoxy-galactosucrose
DE3062467D1 (en) * 1979-12-20 1983-04-28 Tate & Lyle Plc Process for the preparation of 4,1',6'-trichloro-4,1',6'-trideoxy-galactosucrose
EP0043649B1 (en) * 1980-07-08 1984-09-12 TATE & LYLE PUBLIC LIMITED COMPANY Process for the preparation of 4, 1',6'-trichloro-4,1',6'-trideoxygalactosucrose (tgs)

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
glycopyranosides via cyclic tin intermediates" *

Also Published As

Publication number Publication date
KR0143234B1 (ko) 1998-07-01
YU47159B (sh) 1995-01-31
YU139389A (en) 1991-02-28
FI893455A0 (fi) 1989-07-17
DK170027B1 (da) 1995-05-01
EP0352048A2 (en) 1990-01-24
US4950746A (en) 1990-08-21
NO892926L (no) 1990-01-19
JP2725710B2 (ja) 1998-03-11
DE68919566T2 (de) 1995-04-13
NO892926D0 (no) 1989-07-17
MX16842A (es) 1993-04-01
DK352689D0 (da) 1989-07-17
JPH0273096A (ja) 1990-03-13
MX172793B (es) 1994-01-13
DK352689A (da) 1990-01-19
GR1002250B (en) 1996-04-23
AU618107B2 (en) 1991-12-12
IL91004A0 (en) 1990-02-09
ES2065386T3 (es) 1995-02-16
EP0352048A3 (en) 1991-09-04
KR910002884A (ko) 1991-02-26
PT91186A (pt) 1990-02-08
NZ229823A (en) 1991-01-29
ZA895427B (en) 1991-03-27
PT91186B (pt) 1995-03-01
NO171855C (no) 1993-05-12
IL91004A (en) 1994-04-12
AR245136A1 (es) 1993-12-30
GR890100456A (el) 1990-06-27
IE892310L (en) 1990-01-18
FI91874B (fi) 1994-05-13
AU3804889A (en) 1990-01-18
RU2041233C1 (ru) 1995-08-09
IE65990B1 (en) 1995-11-29
FI91874C (fi) 1994-08-25
DE68919566D1 (de) 1995-01-12
TR27628A (tr) 1995-06-14
CA1323625C (en) 1993-10-26
PH26098A (en) 1992-02-06
NO171855B (no) 1993-02-01
FI893455A (fi) 1990-01-19
ATE114664T1 (de) 1994-12-15

Similar Documents

Publication Publication Date Title
EP0352048B1 (en) Process for synthesizing sucrose derivatives by regioselective reaction
EP0454386B1 (en) Sucrose-6-ester production process
EP0448413B1 (en) Selective 6-acylation of sucrose mediated by cyclic adducts of dialkyltin oxides and diols
EP0455390B1 (en) Process for delivery of organotin esters from reaction mixtures containing the same and re-use of the recovered organotin compounds
JPH04225993A (ja) サツカロース−６−エステルの製造法
US20090105470A1 (en) Tin Mediated Regioselective Synthesis of Sucrose-6-Esters
CA2049886C (en) Catalyzed sucrose-6-ester process
US5792842A (en) Ganglioside GM3 derivative having fluorine atom at 9-position of sialic acid and intermediates therefor
EP0389110B1 (en) Process for the preparation of 2'-deoxy-5-trifluoromethyl-beta-uridine
US4914195A (en) Process for preparing N-acetylneuraminic acid derivatives
AU712905B2 (en) High yield stereospecific mannosylation
EP0373919B1 (en) Process for the preparation of 2'-deoxy-beta-adenosine
JPH06135983A (ja) 高級アルキルグリコシドの製造方法およびその中間体
EP0114331A1 (en) A process for preparing oxanosine
JPH04225992A (ja) 新規白金錯体

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE CH DE ES FR GB IT LI LU NL SE

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE CH DE ES FR GB IT LI LU NL SE

17P Request for examination filed

Effective date: 19920211

17Q First examination report despatched

Effective date: 19940124

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE ES FR GB IT LI LU NL SE

REF Corresponds to:

Ref document number: 114664

Country of ref document: AT

Date of ref document: 19941215

Kind code of ref document: T

REF Corresponds to:

Ref document number: 68919566

Country of ref document: DE

Date of ref document: 19950112

ET Fr: translation filed
REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2065386

Country of ref document: ES

Kind code of ref document: T3

ITF It: translation for a ep patent filed

Owner name: SOCIETA' ITALIANA BREVETTI S.P.A.

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: LU

Payment date: 20010706

Year of fee payment: 13

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20010711

Year of fee payment: 13

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 20010713

Year of fee payment: 13

REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020717

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020717

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020731

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020731

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20030707

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20030730

Year of fee payment: 15

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040718

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20050201

EUG Se: european patent has lapsed
NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 20050201

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20080821

Year of fee payment: 20

Ref country code: DE

Payment date: 20080724

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20080718

Year of fee payment: 20

Ref country code: IT

Payment date: 20080730

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20080723

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20090126

Year of fee payment: 20

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

Expiry date: 20090716

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20090718

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20090718

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20090716